US11925916B2 - Method and composition for removing uremic toxins - Google Patents
Method and composition for removing uremic toxins Download PDFInfo
- Publication number
- US11925916B2 US11925916B2 US16/203,058 US201816203058A US11925916B2 US 11925916 B2 US11925916 B2 US 11925916B2 US 201816203058 A US201816203058 A US 201816203058A US 11925916 B2 US11925916 B2 US 11925916B2
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- US
- United States
- Prior art keywords
- sorbent
- titanium
- glyoxal
- urea
- activated carbon
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- 238000000034 method Methods 0.000 title claims abstract description 24
- 239000000203 mixture Substances 0.000 title claims abstract description 15
- 239000002441 uremic toxin Substances 0.000 title description 5
- 239000002594 sorbent Substances 0.000 claims abstract description 170
- FVYDHKPVFSZZAX-UHFFFAOYSA-N oxaldehyde;titanium Chemical compound [Ti].O=CC=O FVYDHKPVFSZZAX-UHFFFAOYSA-N 0.000 claims abstract description 69
- 239000000385 dialysis solution Substances 0.000 claims abstract description 51
- 238000000502 dialysis Methods 0.000 claims abstract description 37
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 228
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 150
- 239000004202 carbamide Substances 0.000 claims description 148
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical group O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 claims description 52
- 239000000463 material Substances 0.000 claims description 43
- 239000012530 fluid Substances 0.000 claims description 31
- 229940015043 glyoxal Drugs 0.000 claims description 25
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 20
- 238000001179 sorption measurement Methods 0.000 claims description 17
- 239000010936 titanium Substances 0.000 claims description 15
- 229910052719 titanium Inorganic materials 0.000 claims description 13
- 108010046334 Urease Proteins 0.000 claims description 12
- 229910021389 graphene Inorganic materials 0.000 claims description 12
- VHZFWWBVRWWSEI-UHFFFAOYSA-N oxaldehyde;zirconium Chemical compound [Zr].O=CC=O VHZFWWBVRWWSEI-UHFFFAOYSA-N 0.000 claims description 11
- 239000011148 porous material Substances 0.000 claims description 10
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 9
- 238000004891 communication Methods 0.000 claims description 8
- 229910021426 porous silicon Inorganic materials 0.000 claims description 8
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 8
- JUWGUJSXVOBPHP-UHFFFAOYSA-B titanium(4+);tetraphosphate Chemical compound [Ti+4].[Ti+4].[Ti+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O JUWGUJSXVOBPHP-UHFFFAOYSA-B 0.000 claims description 8
- -1 titanium ions Chemical class 0.000 claims description 7
- LCKIEQZJEYYRIY-UHFFFAOYSA-N Titanium ion Chemical compound [Ti+4] LCKIEQZJEYYRIY-UHFFFAOYSA-N 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 6
- 239000004408 titanium dioxide Substances 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000003556 assay Methods 0.000 claims 2
- 230000008929 regeneration Effects 0.000 abstract description 3
- 238000011069 regeneration method Methods 0.000 abstract description 3
- 239000000243 solution Substances 0.000 description 20
- 229910052799 carbon Inorganic materials 0.000 description 16
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 102100035309 GRIP and coiled-coil domain-containing protein 1 Human genes 0.000 description 12
- 101001024398 Homo sapiens GRIP and coiled-coil domain-containing protein 1 Proteins 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000002699 waste material Substances 0.000 description 10
- 238000001631 haemodialysis Methods 0.000 description 9
- 230000000322 hemodialysis Effects 0.000 description 9
- NNTWKXKLHMTGBU-UHFFFAOYSA-N 4,5-dihydroxyimidazolidin-2-one Chemical compound OC1NC(=O)NC1O NNTWKXKLHMTGBU-UHFFFAOYSA-N 0.000 description 8
- 210000004369 blood Anatomy 0.000 description 7
- 239000008280 blood Substances 0.000 description 7
- 238000011282 treatment Methods 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 239000003053 toxin Substances 0.000 description 5
- 231100000765 toxin Toxicity 0.000 description 5
- 108700012359 toxins Proteins 0.000 description 5
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- DDRJAANPRJIHGJ-UHFFFAOYSA-N creatinine Chemical compound CN1CC(=O)NC1=N DDRJAANPRJIHGJ-UHFFFAOYSA-N 0.000 description 4
- 239000000004 hemodialysis solution Substances 0.000 description 4
- 230000001172 regenerating effect Effects 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 229910052710 silicon Inorganic materials 0.000 description 4
- 239000010703 silicon Substances 0.000 description 4
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 4
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 210000004379 membrane Anatomy 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 210000003200 peritoneal cavity Anatomy 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000012085 test solution Substances 0.000 description 3
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 208000001647 Renal Insufficiency Diseases 0.000 description 2
- 101100273916 Schizosaccharomyces pombe (strain 972 / ATCC 24843) wip1 gene Proteins 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 229910003074 TiCl4 Inorganic materials 0.000 description 2
- LEHOTFFKMJEONL-UHFFFAOYSA-N Uric Acid Chemical compound N1C(=O)NC(=O)C2=C1NC(=O)N2 LEHOTFFKMJEONL-UHFFFAOYSA-N 0.000 description 2
- TVWHNULVHGKJHS-UHFFFAOYSA-N Uric acid Natural products N1C(=O)NC(=O)C2NC(=O)NC21 TVWHNULVHGKJHS-UHFFFAOYSA-N 0.000 description 2
- PNNCWTXUWKENPE-UHFFFAOYSA-N [N].NC(N)=O Chemical compound [N].NC(N)=O PNNCWTXUWKENPE-UHFFFAOYSA-N 0.000 description 2
- 239000001099 ammonium carbonate Substances 0.000 description 2
- 235000012501 ammonium carbonate Nutrition 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- XFVGXQSSXWIWIO-UHFFFAOYSA-N chloro hypochlorite;titanium Chemical compound [Ti].ClOCl XFVGXQSSXWIWIO-UHFFFAOYSA-N 0.000 description 2
- 229940109239 creatinine Drugs 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 201000006370 kidney failure Diseases 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 2
- 239000003330 peritoneal dialysis fluid Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- ZWYDDDAMNQQZHD-UHFFFAOYSA-L titanium(ii) chloride Chemical compound [Cl-].[Cl-].[Ti+2] ZWYDDDAMNQQZHD-UHFFFAOYSA-L 0.000 description 2
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 description 2
- 229940045136 urea Drugs 0.000 description 2
- 229940116269 uric acid Drugs 0.000 description 2
- SPFMQWBKVUQXJV-BTVCFUMJSA-N (2r,3s,4r,5r)-2,3,4,5,6-pentahydroxyhexanal;hydrate Chemical compound O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O SPFMQWBKVUQXJV-BTVCFUMJSA-N 0.000 description 1
- CYDQOEWLBCCFJZ-UHFFFAOYSA-N 4-(4-fluorophenyl)oxane-4-carboxylic acid Chemical compound C=1C=C(F)C=CC=1C1(C(=O)O)CCOCC1 CYDQOEWLBCCFJZ-UHFFFAOYSA-N 0.000 description 1
- 208000037157 Azotemia Diseases 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910006130 SO4 Inorganic materials 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 239000008121 dextrose Substances 0.000 description 1
- 229960001795 dextrose hydrous Drugs 0.000 description 1
- 238000011026 diafiltration Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 229960001031 glucose Drugs 0.000 description 1
- 238000002615 hemofiltration Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- FUBACIUATZGHAC-UHFFFAOYSA-N oxozirconium;octahydrate;dihydrochloride Chemical compound O.O.O.O.O.O.O.O.Cl.Cl.[Zr]=O FUBACIUATZGHAC-UHFFFAOYSA-N 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000003880 polar aprotic solvent Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000003586 protic polar solvent Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 210000005227 renal system Anatomy 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000001540 sodium lactate Substances 0.000 description 1
- 229940005581 sodium lactate Drugs 0.000 description 1
- 235000011088 sodium lactate Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000001519 tissue Anatomy 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000013638 trimer Substances 0.000 description 1
- ZJHHPAUQMCHPRB-UHFFFAOYSA-N urea urea Chemical compound NC(N)=O.NC(N)=O ZJHHPAUQMCHPRB-UHFFFAOYSA-N 0.000 description 1
- 208000009852 uremia Diseases 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 229910001928 zirconium oxide Inorganic materials 0.000 description 1
- 229910000166 zirconium phosphate Inorganic materials 0.000 description 1
- LEHFSLREWWMLPU-UHFFFAOYSA-B zirconium(4+);tetraphosphate Chemical compound [Zr+4].[Zr+4].[Zr+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LEHFSLREWWMLPU-UHFFFAOYSA-B 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/223—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0211—Compounds of Ti, Zr, Hf
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M1/00—Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
- A61M1/14—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
- A61M1/16—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
- A61M1/1694—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes with recirculating dialysing liquid
- A61M1/1696—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes with recirculating dialysing liquid with dialysate regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3204—Inorganic carriers, supports or substrates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3244—Non-macromolecular compounds
- B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
- B01J20/3248—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M1/00—Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
- A61M1/14—Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
- A61M1/28—Peritoneal dialysis ; Other peritoneal treatment, e.g. oxygenation
- A61M1/282—Operational modes
- A61M1/284—Continuous flow peritoneal dialysis [CFPD]
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/50—Aspects relating to the use of sorbent or filter aid materials
- B01J2220/62—In a cartridge
Definitions
- the disclosure relates generally to dialysis processes, and more particularly to sorbents, cartridges containing the sorbents, and methods and systems for using the cartridges in dialysis.
- Renal failure leads to an imbalance of water and minerals (e.g., Na, K, Cl, Ca, P, Mg, SO 4 ) in the body, as well as impaired excretion of the daily metabolic load of fixed hydrogen ions.
- water and minerals e.g., Na, K, Cl, Ca, P, Mg, SO 4
- end products of nitrogen metabolism including urea, creatinine, and uric acid can accumulate in the blood and tissues.
- Dialysis processes have been devised for the separation of elements in a solution by diffusion across a semi-permeable membrane via a concentration gradient. Principally, dialysis in the United States comprises two methods: hemodialysis and peritoneal dialysis.
- Hemodialysis (“HD”) treatment utilizes the patient's blood, HD dialysis fluid, and a dialyzer to remove waste, toxins, and excess water from the patient.
- the patient is connected to a hemodialysis machine and the patient's blood is pumped through the dialyzer and back to the patient.
- Catheters are inserted into the patient's veins and arteries to allow blood flow to and from the dialyzer. Waste, toxins, and excess water are removed from the patient's blood into the HD dialysis fluid by diffusion and/or filtration and the blood is infused back into the patient.
- Hemodialysis treatments last several hours and are generally performed in a treatment center about three or four times per week, although some methods allowing overnight daily treatment at a patient's home have been proposed.
- PD Peritoneal dialysis
- PD dialysis uses a PD dialysis solution, which is infused into a patient's peritoneal cavity.
- the PD dialysis fluid contacts the patient's peritoneal membrane in the peritoneal cavity.
- Waste, toxins, and excess water pass from the patient's bloodstream through the peritoneal membrane and into the dialysis fluid during a specified dwell time via diffusion and osmosis.
- Spent dialysis fluid is then drained from the patient's peritoneal cavity to remove the waste, toxins, and water from the patient.
- the treatment can be repeated several times during the day or overnight, or both, to achieve the desired level of waste, toxin, and excess water removal.
- sorbents can be used to remove waste from the spent dialysis fluid, thereby regenerating the spent dialysis fluid for reuse. Dialysate regeneration advantageously reduces the overall volume of dialysis solution required for dialysis treatment.
- Sorbent materials include zirconium phosphate and zirconium oxide as ion exchange sorbents to remove cationic and/or anionic waste, and are disclosed, for example, in U.S. Patent Publication No. 2014/0001112.
- Other sorbent materials include a zirconium-glyoxal complex coated on activated carbon as described in U.S. Patent Publication No. 2014/0336568.
- the disclosure provides a sorbent comprising titanium-glyoxal complex and a porous support material such as activated carbon.
- the porous support material comprises activated carbon, graphene, graphene oxide, silicon, porous silicon, or a combination thereof.
- the titanium-glyoxal complex comprises titanium-crosslinked hydrated glyoxal moieties.
- the titanium-glyoxal complex is formed by reacting hydrated glyoxal with titanium ions.
- the titanium-glyoxal complex has a structure comprising a molecule of formula I, formula II, formula III, formula IV, or a combination thereof:
- the titanium-glyoxal complex is associated with, adhered to, adsorbed on, coated on, and/or immobilized on the porous support material such as activated carbon.
- the titanium-glyoxal complex is present in pores of the porous support material such as activated carbon.
- the sorbent has urea capacity of greater than about 50 mg urea/g sorbent, such as greater than about 60 mg/g, greater than about 70 mg/g, greater than about 75 mg/g, greater than about 80 mg/g, greater than about 90 mg/g, about 50 mg/g to about 200 mg/g, about 50 mg/g to about 150 mg/g, about 50 mg/g to about 100 mg/g, about 60 mg/g to about 100 mg/g, about 70 mg/g to about 90 mg/g, about 75 mg/g to about 85 mg/g, and/or about 80 mg/g.
- urea capacity of greater than about 50 mg urea/g sorbent, such as greater than about 60 mg/g, greater than about 70 mg/g, greater than about 75 mg/g, greater than about 80 mg/g, greater than about 90 mg/g, about 50 mg/g to about 200 mg/g, about 50 mg/g to about 150 mg/g, about 50 mg/g to about 100 mg/g, about 60 mg/g to about 100
- the molar ratio of titanium to glyoxal is about 1:4.
- the disclosure provides a sorbent cartridge comprising a sorbent according to any other embodiment listed herein.
- the sorbent cartridge is free of an immobilized urease layer.
- total content of active urease in the sorbent cartridge is less than about 5 wt. % based on total immobilized weight portion of cartridge contents.
- the sorbent cartridge further comprises dialysate fluid which communicates with the sorbent.
- the dialysate fluid has a pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- the sorbent cartridge further comprises a layer comprising titanium oxide, hydrous titanium dioxide, and/or titanium phosphate.
- the disclosure provides a method comprising passing a fluid comprising urea though the sorbent according to any other embodiment listed herein and/or though the sorbent cartridge according to any other embodiment listed herein, thereby binding urea to the titanium-glyoxal complex.
- the fluid comprising urea is a spent dialysis fluid.
- the fluid comprising urea has a pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- the disclosure provides an apparatus for conducting dialysis comprising the sorbent cartridge according to any other embodiment listed herein, and a dialyzer in fluid communication with the sorbent cartridge, wherein spent dialysis fluid passes from the dialyzer to and through the sorbent cartridge.
- the spent dialysis fluid is spent hemodialysis fluid or spent peritoneal dialysis fluid.
- the dialyzer is in fluid communication with the blood of a patient.
- the disclosure provides a dialysis system comprising the sorbent cartridge of any other embodiment listed herein and a source of spent dialysis fluid, wherein the source of spent dialysis fluid is in fluid communication with the sorbent cartridge and the spent dialysis fluid passes to and through the sorbent cartridge.
- the spent dialysis fluid is spent hemodialysis fluid or spent peritoneal dialysis fluid.
- the disclosure provides a method of making a sorbent for binding urea, comprising: (i) combining glyoxal, a titanium ion source, and a solvent to provide a mixture comprising a titanium-glyoxal complex; (ii) adding a porous support material to the mixture to provide a treated support material; (iii) separating the solvent from the treated support material; (iv) washing the treated support material to provide a washed treated support material; and (v) drying the washed treated support material to provide a sorbent for binding urea.
- the porous support material comprises activated carbon, graphene, graphene oxide, silicon, porous silicon, or a combination thereof.
- the disclosure provides a method of making a sorbent for binding urea, comprising: (i) combining glyoxal, a titanium ion source, and a solvent to provide a mixture comprising a titanium-glyoxal complex; (ii) adding activated carbon to the mixture to provide a treated activated carbon; (iii) separating the solvent from the treated activated carbon; (iv) washing the treated activated carbon to provide a washed treated activated carbon; and (v) drying the washed treated activated carbon to provide a sorbent for binding urea.
- the drying step is carried out at a temperature of at least 25° C., such as at least 30° C., at least 35° C., at least 40° C., about 25° C. to about 40° C., about 30° C. to about 40° C., about 35° C. to about 40° C., and/or about 37° C.
- the titanium ion source is selected from the group consisting of titanium tetrachloride, titanium (II) chloride, titanium (III) chloride, titanium oxychloride, and combinations thereof.
- FIG. 1 illustrates an embodiment of a cross-sectional view of a resin bed of a cartridge as disclosed herein.
- Certain embodiments described herein relate generally to the field of dialysis processes. More particularly, some embodiments described herein relate to sorbents for use in dialysis processes to remove waste products such as uremic toxins that accumulate in dialysis fluids. Related embodiments described herein relate to cartridges containing the sorbents. Additional related embodiments described herein relate to methods and systems for using the cartridges in dialysis processes.
- the sorbents, sorbent cartridges, methods, and systems described herein are useful for the removal of waste products (e.g., uremic toxins) that accumulate in dialysate fluids.
- the sorbent materials can be present in a container (e.g., one or more sorbent cartridges) capable of holding the sorbents useful for the removal process.
- the sorbents described in detail below, or the arrangement of sorbents can be used in a dialysis system or other similar type of system that is useful for the removal of waste products that accumulate in dialysate fluids, for instance, as a result of conducting hemodialysis or peritoneal dialysis.
- the sorbents and sorbent cartridges are useful in purifying or regenerating dialysate used in hemodialysis and in peritoneal dialysis.
- Conventional dialysis solutions for peritoneal dialysis or hemodialysis can be used and can advantageously be regenerated by the described methods.
- the sorbents, sorbent cartridges, methods and systems described herein are useful for removing uremic toxins from a patient by dialysis with non-enzymatic urea-binding sorbent materials.
- the non-enzymatic urea-binding sorbent material can be used in one or more sorbent cartridges for dialysate regeneration or purification in dialysis.
- the sorbent cartridge(s) can be used for treatment of uremia and/or other conditions.
- the sorbent material and sorbent cartridge described herein can reduce or avoid generation of ammonia during urea removal because of the absence of enzymatic hydrolysis reactions of urea that are related to conventional use of urease.
- a sorbent material comprising titanium described herein can efficiently adsorb urea at or near a physiological pH, eliminating the need to adjust the pH of the spent dialysis fluid before exposure to the sorbent material and of the purified or regenerated dialysis fluid after exposure to the sorbent material.
- the sorbents disclosed herein comprise a titanium-glyoxal complex and a porous support material.
- the porous support material can comprise activated carbon, graphene, graphene oxide, silicon, porous silicon, or a combination thereof.
- the molar ratio of titanium to glyoxal in the sorbent can be about 1:4.
- the titanium-glyoxal complex can comprise titanium-crosslinked hydrated glyoxal moieties.
- the titanium-glyoxal complex can have a structure comprising a molecule of formula I, formula II, formula III, formula IV, or a combination thereof:
- the titanium-glyoxal complex also includes titanium-glyoxal polymeric complexes having the structure Ti[hydrated glyoxal moiety] n , wherein n is an integer from 2 to 10, such as from 2 to 8, from 2 to 6, from 3 to 5, or 4.
- hydrated glyoxal includes oligomeric and polymeric species of hydrated glyoxal, such as hydrated glyoxal dimers, hydrated glyoxal trimers, hydrated glyoxal oligomers, and hydrated glyoxal polymers.
- the titanium-glyoxal complex described herein can be formed, for example, by reacting hydrated glyoxal with titanium ions.
- a urea-binding sorbent can be formed by treating a support material as described herein (e.g., activated carbon) with the titanium-glyoxal complex.
- the titanium-glyoxal complex can be associated with, adhered to, adsorbed on, and/or coated on the support material such as activated carbon.
- the titanium-glyoxal complex is trapped within pores of the support material or otherwise immobilized to the support material, for example, the titanium-glyoxal complex is trapped within carbon pores or otherwise immobilized to the carbon.
- Urea-containing (e.g., spent) dialysate can be passed through a layer of the formed sorbent to complex urea with the sorbent, thereby purifying or regenerating the spent dialysis fluid.
- sorbents described herein are active toward urea adsorption and are capable of providing adequate urea binding capacity sufficient to eliminate the need for including an immobilized urease layer or similar-acting enzyme in the sorbent cartridge.
- a cartridge “free of an immobilized urease layer” refers to the absence in the cartridge of any stationary continuous layer of urease extending across an internal cross-section thereof that is available for fluid flow. Further, the cartridge of the present invention can be substantially free or completely free of any active urease in the fluid flow compartment of the cartridge.
- the total content of active urease in the fluid flow compartment of the cartridge can be less than about 5 wt % based on the total immobilized weight portion of the cartridge contents, for example, less than about 3 wt %, less than about 2 wt %, less than about 1 wt %, less than about 0.5 wt %, less than 0.1 wt %, and/or from 0 to about 5 wt % based on the total immobilized weight portion of the cartridge contents.
- the sorbents described herein are capable of urea adsorption at or near physiological pH, which eliminates the need to acidify spent dialysis fluid entering the sorbent cartridge and to neutralize the regenerated dialysate exiting from the sorbent cartridge before the dialysate is reused in a dialyzer.
- the pH of dialysate fluid which communicates with the sorbent does not need to be adjusted (e.g., acidified) prior to reaction with the urea-binding sorbent, and thus also does not need to be restored to a neutral pH upon exiting the sorbent cartridge.
- the dialysis fluid which communicates with the sorbent can have a pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- the pH of the purified or regenerated dialysate fluid exiting the sorbent cartridge can have a pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- Activated carbon is one support material that, by itself, has very low adsorption capacity for urea but can be converted into an active urea sorbent, for example, by loading carbon with a titanium-glyoxal complex, such as glyoxal crosslinked by titanium.
- Activated carbon can be converted into a direct urea binding active material by treating carbon with a solution containing titanium-glyoxal complex.
- the glyoxal can be crosslinked with titanium ions to form a titanium crosslinked polymeric complex which can be trapped within carbon pores or otherwise immobilized to the carbon.
- the crosslinked titanium-glyoxal complex can be formed and trapped within the carbon pores, for example, upon drying of the treated carbon.
- the crosslinked titanium-glyoxal polymeric complex of the treated carbon can bind with the urea, which then is captured by the treated carbon.
- the dried treated carbon becomes urea binding active and can attain urea adsorption capacity, such as greater than about 50 mg urea per g treated carbon, e.g., greater than about 60 mg/g, greater than about 70 mg/g, greater than about 75 mg/g, greater than about 80 mg/g, greater than about 90 mg/g, about 50 mg/g to about 200 mg/g, about 50 mg/g to about 150 mg/g, about 50 mg/g to about 100 mg/g, about 60 mg/g to about 100 mg/g, about 70 mg/g to about 90 mg/g, about 75 mg/g to about 85 mg/g, and/or about 80 mg/g.
- urea adsorption capacity such as greater than about 50 mg urea per g treated carbon, e.g., greater than about 60 mg/g, greater than about 70 mg/g, greater than about 75 mg/g, greater than about 80 mg/g, greater than about 90 mg/g, about 50 mg/g to about 200 mg/g, about 50 mg/g
- Urea-binding capacity can be measured in a column test by passing a dialysate containing urea through the column.
- the urea-binding carbons can avoid or reduce the indicated possible problems associated with sorbent material that uses the enzyme urease to convert the urea to ammonium carbonate, in a safe and possibly cost-reducing manner.
- the resultant urea binding carbon can be combined with additional titanium sorbents such as titanium phosphate, titanium oxide, and/or hydrous titanium dioxide in the form of a sorbent cartridge for sorbent regenerative dialysis to remove various uremic toxins from the patient (urea, creatinine, uric acid, phosphate, potassium, calcium etc.).
- the regenerated dialysate is highly pure and uniform in composition allowing the dialysis system to be greatly simplified. Further, since the titanium-glyoxal complex can efficiently adsorb urea at physiological pH, pH adjustment of the spent dialysis fluid and of the purified or regenerated dialysate is minimal or not needed.
- the urea-binding sorbent can be present as a layer (or layers) in a sorbent cartridge, and additional sorbents, including additional titanium sorbents such as titanium phosphate, titanium oxide, and/or hydrous titanium dioxide can be present as additional layers in the sorbent cartridge.
- the sorbent layer which comprises the urea-binding titanium-glyoxal complex can be used in an amount, for example, of from about 500 to about 2000 g per dialysis cartridge, such as from about 1000 to about 2000 g treated carbon per cartridge (or other amounts above or below these ranges) used in hemodialysis, or from about 750 to about 1250 g per cartridge (or other amounts above or below these ranges) used in peritoneal dialysis.
- Additional layers optionally can be included in the cartridge before, and/or after the sorbent layer comprising the titanium glyoxal complex, such as a layer comprising titanium oxide, a layer comprising titanium phosphate, and/or a layer comprising hydrous titanium dioxide.
- the urea-binding sorbent described herein can be prepared by (i) combining glyoxal, a titanium ion source, and a solvent to provide a mixture comprising a titanium-glyoxal complex; and (ii) adding a porous support material such as activated carbon, graphene, graphene oxide, silicon, porous silicon, or a combination thereof to the mixture to provide a treated support material (e.g., a treated activated carbon).
- a porous support material such as activated carbon, graphene, graphene oxide, silicon, porous silicon, or a combination thereof
- the titanium-glyoxal complex is thereby associated with, adhered to, adsorbed on, coated on, immobilized on, and/or present in pores of the support material such as activated carbon.
- the solvent can include, but is not limited to, water and organic solvents such as polar protic solvents and polar aprotic solvents.
- the solvent can be separated from the treated support material (e.g., the treated activated carbon), the treated support material (e.g., treated activated carbon) can be washed to provide a washed treated support material (e.g., a washed treated activated carbon); and/or the washed treated support material (e.g., washed, treated activated carbon) can be dried to provide a dried sorbent for binding urea.
- the solution for washing the treated support material can include, but is not limited to water or acidic solutions, such as hydrochloric acid solutions (e.g., 3.5 N HCl solution).
- the titanium ion source can be titanium tetrachloride, titanium (II) chloride, titanium (III) chloride, titanium oxychloride, and combinations thereof.
- the drying step can be carried out at a temperature of at least 25° C., such as at least 30° C., at least 35° C., at least 40° C., about 25° C. to about 40° C., about 30° C. to about 40° C., about 35° C. to about 40° C., and/or about 37° C.
- the sorbents and sorbent cartridges described herein can be used in a process for removing urea from a fluid, such as in a process that purifies and/or regenerates spent dialysis fluid, which also includes urea removal.
- the process can include passing a fluid comprising urea through the urea-binding sorbent and the sorbent cartridges containing a urea-binding sorbent as described herein, thereby binding urea to the titanium-glyoxal complex of the urea-binding sorbent.
- the process can comprise running spent (e.g., urea-containing) dialysis fluid through the sorbent or cartridge.
- the cartridge can comprise the titanium-glyoxal complex which is bound to a porous support material (e.g., activated carbon) in a sorbent layer.
- a porous support material e.g., activated carbon
- the titanium-glyoxal complex can be associated with, adhered to, adsorbed on, coated on, immobilized on, and/or present in the pores of the support material (e.g., activated carbon).
- Spent dialysis fluid then can be passed through the sorbent layer loaded with the insolubilized titanium-glyoxal complex.
- the insolubilized titanium-glyoxal complex can be used as a urea binder itself, without need of additional urea binding materials.
- Additional layers through which the spent dialysis fluid passes optionally can be included in the cartridge before, and/or after the sorbent layer comprising the titanium glyoxal complex.
- Such layers can include a layer comprising titanium oxide, a layer comprising titanium phosphate, a layer comprising hydrous titanium dioxide, or a combination thereof, such as a layer comprising both titanium oxide and titanium phosphate.
- Such layers collectively comprise a resin bed of a cartridge as disclosed herein.
- FIG. 1 illustrates an embodiment of a cross-sectional view of a resin bed 10 as disclosed herein.
- the resin bed 10 in the illustrated embodiment includes three layers 20 , 22 , and 24 .
- the first layer 20 is a layer comprising titanium phosphate.
- the second layer 22 is a layer comprising titanium oxide.
- the third layer 24 is a layer comprising titanium-glyoxal complex. Fluid passes through the layers in the directed indicated by the arrows. Additional layers may be included in the sorbent cartridge and the layers in the sorbent cartridge may be provided in any order.
- the fluid before contacting the urea-binding sorbent or entering the sorbent cartridge, can have a pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- a pH of about 5 to about 9 such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- the fluid can have a similar pH of about 5 to about 9, such as about 5.5 to about 8.5, about 6 to about 8, about 6.1 to about 7.9, about 6.2 to about 7.8, about 6.3 to about 7.7, about 6.4 to about 7.6, about 6.5 to about 7.5, about 6.6 to about 7.4, about 6.7 to about 7.3, about 6.8 to about 7.2, about 6.9 to about 7.1, and/or about 7.
- the sorbents and sorbent cartridges described herein can be used in an apparatus for conducting dialysis, so as to purify and/or regenerate spent dialysis fluid.
- the apparatus can comprise a sorbent cartridge as described herein and a dialyzer in fluid communication with the sorbent cartridge, wherein spent dialysis fluid passes from the dialyzer to and through the sorbent cartridge.
- the spent dialysis fluid can be spent hemodialysate, spent peritoneal dialysate, spent hemofiltration fluid or spent diafiltration fluid.
- the dialyzer can be in fluid communication with the blood of a patient.
- the apparatus for conducting dialysis can be, for example, an apparatus for sorbent hemodialysis, a wearable artificial kidney, or an apparatus for sorbent peritoneal dialysis.
- the sorbents and sorbent cartridges described herein can be used in a dialysis system, so as to purify and/or regenerate spent dialysis fluid.
- the dialysis system can comprise a sorbent cartridge as described herein and a source of spent dialysis fluid, wherein the source of spent dialysis fluid is in fluid communication with the sorbent cartridge and the spent dialysis fluid passes to and through the sorbent cartridge.
- the spent dialysis fluid can be spent hemodialysate, spent peritoneal dialysate, or others listed above.
- the spent dialysis fluid can pass through the sorbent cartridge at a rate, for example, of about 10 ml/min to about 1000 ml/min, about 100 ml/min to about 550 ml/min, and/or about 150 ml/min to about 400 ml/min.
- the dialysis system can regenerate the spent dialysis fluid without needing to adjust the pH of the spent dialysis fluid, and can regenerate the spent dialysis fluid to a pH level approximately equal to that of fresh dialysate.
- the system can also regenerate the spent dialysis fluid without the formation of ammonia.
- Titanium-glyoxal complex was prepared as shown in Scheme 1 by adding 4.87 g TiCl 4 (99% purity) to 15.28 g glyoxal (39% glyoxal in water). The mixture was stirred for about 20 minutes and the reaction flask was immersed in an ice bath as needed to obtain the titanium glyoxal complex in a mole ratio of TiCl 4 :glyoxal of 1:4.
- Activated carbon was coated with the titanium-glyoxal complex prepared according to Example 1 by adding about 10 g of the titanium-glyoxal solution to about 5 g of activated carbon (AC) as shown in Table 1:
- Ti-Gly-AC titanium-glyoxal-activated carbon
- urea sorption by the titanium-glyoxal complex-coated activated carbon 1 g was added to a 50 mL centrifuge tube. Next, 50 ml of peritoneal dialysis (PD) solution containing urea (60 mg/dL or 257 mg/dL urea/PD solution) was added to the tubes.
- PD peritoneal dialysis
- Each 100 ml of the DIANEAL® Low Calcium (2.5 mEq/L) Peritoneal Dialysis Solution with 2.5% Dextrose contains 2.5 g dextrose hydrous USP, 538 mg sodium chloride USP, 448 mg sodium lactate, 18.3 mg calcium chloride USP, and 5.08 mg magnesium chloride USP, and has a pH of about 5.2.
- the tubes were then rotated and liquid samples were collected from the tubes at different time points for urea, chemical analysis and pH.
- a zirconium-glyoxal activated carbon sample was prepared by mixing 35 g of 39% glyoxal aqueous solution together with 75 ml of a 40% aqueous solution of zirconium (IV) oxychloride octahydrate (ZrOCl ⁇ 8H 2 O), then added 50 ml of 5N HCl solution and mixed overnight. Next, 55 mL of the resulting solution was mixed with 20 g of activated carbon for 4 hours, filtered with 150 ml of 3.5 N HCl and dried overnight in oven at 38° C.
- the titanium-glyoxal complex-coated activated carbon demonstrated higher urea sorption capacity than either zirconium glyoxal complex-coated activated carbon or activated carbon alone.
- titanium-glyoxal coated on activated carbon demonstrated a urea capacity of 81.4 mg/g sorbent after 68 hours in a 257 mg/dL urea peritoneal dialysis (PD) solution at pH 4.
- urea capacity for zirconium-glyoxal on activated carbon was 373 mg/g sorbent for the same urea solution.
- zirconium-glyoxal coated on activated carbon had a urea capacity of 12.1 mg/kg (see Table 3), whereas water-rinsed titanium-glyoxal coated on activated carbon demonstrated a higher urea capacity of 41.4 g/kg sorbent after 68 hours in a 257 mg/dL urea peritoneal dialysis (PD) solution at pH 5 (see Table 3). Additionally, as shown in Table 3, titanium-glyoxal coated on activated carbon demonstrated a lower ammonia value compared to zirconium-glyoxal coated on activated carbon.
- Ti-Gly-AC prepared according to Example 2 was added to a 50 mL centrifuge tube.
- 50 ml of 112 mg/dL urea nitrogen dialysis solution was added to the tube.
- the dialysis solution contains: 112 mg/dL BUN, 0.2 mg/dL Ca 2+ , 17 mmol/L bicarbonate, 2.6 mg/dL Mg 2+ , 3.1 mg/dL phosphorous, 130 mmol/L Na + , 3.2 mmol/L K + , and 113 mmol/L Cl ⁇ , and is at pH 8.8.
- Samples that were rinsed, were rinsed with RO water, filtered, and dried at 37° C. The tubes were then rotated and liquid samples were collected from the tubes at different time points for urea, electrolyte analysis and pH.
- Zirconium glyoxal complex-coated activated carbon was prepared as described in Example 3.
- titanium-glyoxal complex-coated activated carbon demonstrated higher urea sorption capacity than either zirconium glyoxal complex-coated activated carbon or activated carbon alone.
- titanium-glyoxal coated on activated carbon demonstrated a urea capacity of 58 mg/g sorbent after 68 hours in a 112 mg/dL urea nitrogen dialysate solution around pH 7.
- urea capacity for zirconium-glyoxal on activated carbon was 11 mg/g sorbent for the same urea solution.
Abstract
Description
TABLE 1 | ||||
Activated | Activated | |||
carbon, | carbon, | |||
CalgonCarbon, | CalgonCarbon, | |||
product: HPC | product: | Ti-Gly-AC | ||
Ti-glyoxal | SuperHD, | OLC AW, | final | |
Sample | complex | 12 × 40 | 12 × 40 | dry weight |
No. | (g) | (“CC1”) (g) | (“CC2”) (g) | (g) |
1 | 9.438 | 5.0016 | — | 7.3527 |
2 | 10.562 | — | 5.036 | 6.7757 |
q=([BUN] i −[BUN] t)×(60/28)×V/100/S
in which:
-
- q is urea capacity in mg urea/g sorbent
- [BUN]i is concentration of BUN in dialysate solution at time 0 in mg/dL
- [BUN]t is concentration of BUN in dialysate solution at time t in mg/dL
- V is volume of test solution in ml
- S is weight of sorbent in g.
TABLE 2 | ||||
Original Zr-Gly-AC |
RUN 2 | RUN 1 |
Urea | Urea | |||||
capacity, | capacity, | |||||
Time, | mg/g | mg/g | ||||
Tube | Sorbent | Test Solution | hr | sorbent | pH | sorbent |
1 | Zr-Glyoxal-AC from CC1 | 257 mg/dL urea/PD | 0.5 | 16.3 | ||
1 | Zr-Glyoxal-AC from CC1 | 257 mg/dL urea/PD | 2 | 18.5 | ||
1 | Zr-Glyoxal-AC from CC1 | 257 mg/dL urea/PD | 67 | 34.4 | 2.24 | 37.3 |
1 | Zr-Glyoxal-AC from CC1 | 257 mg/dL urea/PD | 115 | 38.2 | ||
2 | Zr-Glyoxal-AC from CC2 | 257 mg/dL urea/PD | 0.5 | 15.3 | ||
2 | Zr-Glyoxal-AC from CC2 | 257 mg/dL urea/PD | 2 | 18.9 | ||
2 | Zr-Glyoxal-AC from CC2 | 257 mg/dL urea/PD | 67 | 34.2 | 2.46 | 39.3 |
2 | Zr-Glyoxal-AC from CC2 | 257 mg/dL urea/PD | 115 | 40.9 | ||
3 | Zr-Glyoxal-AC from GCC1 | 257 mg/dL urea/PD | 0.5 | 11.4 | ||
3 | Zr-Glyoxal-AC from GCC1 | 257 mg/dL urea/PD | 2 | 13.5 | ||
3 | Zr-Glyoxal-AC from GCC1 | 257 mg/dL urea/PD | 67 | 24.0 | 3.00 | 26.7 |
3 | Zr-Glyoxal-AC from GCC1 | 257 mg/dL urea/PD | 115 | 28.1 | ||
4 | AC from CC1 | 257 mg/dL urea/PD | 2 | 7.6 | ||
4 | AC from CC1 | 257 mg/dL urea/PD | 67 | 7.3 | 6.40 | |
5 | AC from CC2 | 257 mg/dL urea/PD | 2 | 7.1 | ||
5 | AC from CC2 | 257 mg/dL urea/PD | 67 | 6.9 | 8.36 | |
6 | AC from GCC1 | 257 mg/dL urea/PD | 2 | 7.8 | ||
6 | AC from GCC1 | 257 mg/dL urea/PD | 67 | 5.7 | 5.13 | |
7 | Zr-Glyoxal-AC from CC1 | 60 mg/dL urea/PD | 0.5 | 4.2 | ||
7 | Zr-Glyoxal-AC from CC1 | 60 mg/dL urea/PD | 2 | 5.3 | ||
7 | Zr-Glyoxal-AC from CC1 | 60 mg/dL urea/PD | 67 | 11.9 | 2.18 | 12.5 |
7 | Zr-Glyoxal-AC from CC1 | 60 mg/dL urea/PD | 115 | 14.3 | ||
8 | Zr-Glyoxal-AC from CC2 | 60 mg/dL urea/PD | 0.5 | 4.1 | ||
8 | Zr-Glyoxal-AC from CC2 | 60 mg/dL urea/PD | 2 | 5.7 | ||
8 | Zr-Glyoxal-AC from CC2 | 60 mg/dL urea/PD | 67 | 11.8 | 2.47 | 12.2 |
8 | Zr-Glyoxal-AC from CC2 | 60 mg/dL urea/PD | 115 | 13.7 | ||
9 | Zr-Glyoxal-AC from GCC1 | 60 mg/dL urea/PD | 0.5 | 3.1 | ||
9 | Zr-Glyoxal-AC from GCC1 | 60 mg/dL urea/PD | 2 | 4.0 | ||
9 | Zr-Glyoxal-AC from GCC1 | 60 mg/dL urea/PD | 67 | 9.1 | 2.54 | 8.5 |
9 | Zr-Glyoxal-AC from GCC1 | 60 mg/dL urea/PD | 115 | 10.1 | ||
10 | AC from CC1 | 60 mg/dL urea/PD | 2 | 2.3 | ||
10 | AC from CC1 | 60 mg/dL urea/PD | 67 | 2.0 | 6.10 | |
11 | AC from CC2 | 60 mg/dL urea/PD | 2 | 2.3 | ||
11 | AC from CC2 | 60 mg/dL urea/PD | 67 | 2.3 | 6.75 | |
12 | AC from GCC1 | 60 mg/dL urea/PD | 2 | 1.8 | ||
12 | AC from GCC1 | 60 mg/dL urea/PD | 67 | 2.0 | 6.18 | |
TABLE 3 | |||||||||||||
Urea | |||||||||||||
CA, | Mg, | P, | Na, | K, | CL, | capacity, | |||||||
Test | NH3, | BUN | mg/ | Bicarb, | mg/ | mg/ | mmol/ | mmol/ | mmol/ | Urea, | mg/g | ||
Sorbent | Solution | umol/L | mg/dL | dL | mmol/L | dL | dL | L | L | L | pH | mg/dl | sorbent |
Zr- | 257 | 135.1 | 93 | 5.4 | 0.6 | 1.1 | 0 | 130 | 0.7 | 133 | 2.41 | 199.3 | 24.2 |
Glyoxal- | mg/dL | ||||||||||||
AC from | urea/PD | ||||||||||||
CC1 | |||||||||||||
Zr- | 257 | 476.9 | 90.6 | 4.7 | 0.3 | 0.6 | 0 | 130 | 0.8 | 125 | 2.9 | 194.1 | 27.8 |
Glyoxal- | mg/dL | ||||||||||||
AC from | urea/PD | ||||||||||||
CC2 | |||||||||||||
Ti- | 257 | 117.8 | 37.6 | 6.3 | 0.4 | 1.9 | 0 | 130 | 0.7 | 109 | 4 | 80.6 | 81.4 |
Glyoxal- | mg/dL | ||||||||||||
AC from | urea/PD | ||||||||||||
CC1 | |||||||||||||
Ti- | 257 | 259.9 | 56.4 | 5 | 0.2 | 1.3 | 0.1 | 131 | 1.5 | 110 | 3.9 | 120.9 | 63.0 |
Glyoxal- | mg/dL | ||||||||||||
AC from | urea/PD | ||||||||||||
CC2 | |||||||||||||
Zr- | 257 | 66 | 105.9 | 4.1 | 0.3 | 0.6 | 0 | 131 | 0.7 | 97 | 4.79 | 226.9 | 12.1 |
Glyoxal- | mg/dL | ||||||||||||
AC CC1 | urea/PD | ||||||||||||
rinsed | |||||||||||||
Zr- | 257 | 76.1 | 106 | 4.3 | 0 | 0.6 | 0 | 132 | 0.7 | 97 | 5.04 | 227.1 | 11.9 |
Glyoxal- | mg/dL | ||||||||||||
AC CC2 | urea/PD | ||||||||||||
rinsed | |||||||||||||
Ti- | 257 | 108.5 | 77.6 | 4.9 | 0.5 | 1.2 | 0 | 131 | 0.7 | 99 | 5.01 | 166.3 | 41.4 |
Glyoxal- | mg/dL | ||||||||||||
AC CC1 | urea/PD | ||||||||||||
rinsed | |||||||||||||
Ti- | 257 | 246.6 | 17.7 | 5.4 | 0.1 | 1.1 | 0 | 131 | 0.7 | 113 | 4.83 | 37.9 | 99.7 |
Glyoxal- | mg/dL | ||||||||||||
AC CC2 | urea/PD | ||||||||||||
rinsed | |||||||||||||
Zr- | 60 mg/dL | 729 | 18.3 | 4.7 | 0.4 | 0.6 | 0 | 131 | 0.8 | 126 | 2.58 | 39.2 | 9.8 |
Glyoxal- | urea/PD | ||||||||||||
AC from | |||||||||||||
CC1 | |||||||||||||
Zr- | 60 mg/dL | 711 | 18.9 | 4.6 | 0.4 | 0.6 | 0 | 131 | 0.8 | 127 | 2.73 | 40.5 | 9.2 |
Glyoxal- | urea/PD | ||||||||||||
AC from | |||||||||||||
CC2 | |||||||||||||
Ti- | 60 mg/dL | 138.3 | 6 | 6.2 | 0.4 | 1.9 | 0.1 | 131 | 0.7 | 110 | 3.84 | 12.9 | 22.6 |
Glyoxal- | urea/PD | ||||||||||||
AC from | |||||||||||||
CC1 | |||||||||||||
Ti- | 60 mg/dL | 334.8 | 9.5 | 5 | 0.5 | 1.3 | 0.1 | 132 | 1.6 | 111 | 3.78 | 20.4 | 18.7 |
Glyoxal- | urea/PD | ||||||||||||
AC from | |||||||||||||
CC2 | |||||||||||||
Zr- | 60 mg/dL | 118.5 | 23.6 | 4.1 | 0.5 | 0.6 | 0 | 131 | 0.7 | 97 | 4.58 | 50.6 | 4.4 |
Glyoxal- | urea/PD | ||||||||||||
AC CC1 | |||||||||||||
rinsed | |||||||||||||
Zr- | 60 mg/dL | 115.7 | 24.4 | 4.3 | 0 | 0.6 | 0 | 132 | 0.7 | 96 | 4.68 | 52.3 | 3.6 |
Glyoxal- | urea/PD | ||||||||||||
AC CC2 | |||||||||||||
rinsed | |||||||||||||
Ti- | 60 mg/dL | 94.8 | 11.7 | 5.4 | 0.3 | 1.8 | 0 | 132 | 0.7 | 99 | 5.08 | 25.1 | 16.7 |
Glyoxal- | urea/PD | ||||||||||||
AC CC1 | |||||||||||||
rinsed | |||||||||||||
Ti- | 60 mg/dL | 149.5 | 17 | 4.5 | 0 | 0.9 | 0 | 131 | 0.7 | 98 | 4.75 | 36.4 | 11.1 |
Glyoxal- | urea/PD | ||||||||||||
AC CC2 | |||||||||||||
rinsed | |||||||||||||
257 | 4.1 | 117.4 | 4.7 | 0.1 | 0.6 | 0 | 132 | 0.7 | 93 | 251.6 | |||
mg/dL | |||||||||||||
urea/PD | |||||||||||||
257 | 4.5 | 117.9 | 4.7 | 0 | 0.6 | 0 | 132 | 0.7 | 93 | 252.6 | |||
mg/dL | |||||||||||||
urea/PD | |||||||||||||
60 mg/dl | 2 | 28.1 | 4.6 | 0.2 | 0.6 | 0 | 130 | 0.7 | 92 | 60.2 | |||
urea/PD | |||||||||||||
60 mg/dl | 4.1 | 27.6 | 4.7 | 0 | 0.6 | 0 | 131 | 0.7 | 93 | 59.1 | |||
urea/PD | |||||||||||||
q=([BUN] i −[BUN] t)×(60/28)×V/100/S
in which:
-
- q is urea capacity in mg urea/g sorbent
- [BUN]i is concentration of BUN in dialysate solution at time 0 in mg/dL
- [BUN]t is concentration of BUN in dialysate solution at time t in mg/dL
- V is volume of test solution in ml
- S is weight of sorbent in g.
TABLE 4 | ||||||||||||
Avg Urea | ||||||||||||
capacity, | ||||||||||||
Time, | NH3, | BUN, | CA, | Bicarb, | Mg, | P, | Na, | K, | CL, | mg/g | ||
Sorbent | hr. | umol/L | mg/dL | mg/dL | mmol/L | mg/dL | mg/dL | mmol/L | mmol/L | mmol/L | pH | sorbent |
Zr- | 0.5 | 88.9 | 102.1 | 1 | 0.2 | 3.2 | 1.4 | 129 | 3.2 | 145 | 10.2 | |
Glyoxal- | ||||||||||||
AC from | ||||||||||||
CC1 | ||||||||||||
Zr- | 68 | 79.1 | 96.4 | 1.2 | 0.2 | 3.3 | 0 | 128.5 | 3.2 | 148 | 2.1 | 17.0 |
Glyoxal- | ||||||||||||
AC from | ||||||||||||
CC1 | ||||||||||||
Ti- | 0.5 | 16.8 | 101.1 | 0.4 | 4.1 | 2.7 | 1.9 | 130 | 3.2 | 127 | 11.1 | |
Glyoxal- | ||||||||||||
AC from | ||||||||||||
CC1- | ||||||||||||
new1 | ||||||||||||
Ti- | 68 | 38.9 | 17.3 | 0.5 | 0.2 | 2.7 | 0.7 | 129.5 | 3.2 | 129.5 | 4.8 | 98.6 |
Glyoxal- | ||||||||||||
AC from | ||||||||||||
CC1- | ||||||||||||
new1 | ||||||||||||
ZR- | 0.5 | 9.6 | 102.2 | 0.2 | 13.6 | 2.2 | 2 | 129 | 3.1 | 114 | 10.1 | |
Glyoxal- | ||||||||||||
AC CC1 | ||||||||||||
rinsed | ||||||||||||
ZR- | 68 | 23.9 | 101.8 | 0.2 | 11.4 | 1.7 | 0.2 | 128 | 3.1 | 114.5 | 7.4 | 11.4 |
Glyoxal- | ||||||||||||
AC CC1 | ||||||||||||
rinsed | ||||||||||||
Ti- | 0.5 | 22.6 | 102.1 | 0.2 | 12.9 | 2.5 | 2.5 | 128 | 3.1 | 114 | 10.2 | |
Glyoxal- | ||||||||||||
AC- | ||||||||||||
new1- | ||||||||||||
rinse | ||||||||||||
Ti- | 68 | 67.2 | 57.3 | 0.2 | 10.3 | 2.5 | 1.8 | 129.5 | 3.2 | 115.5 | 7.2 | 58.3 |
Glyoxal- | ||||||||||||
AC- | ||||||||||||
new1- | ||||||||||||
rinse | ||||||||||||
AC from | 0.5 | 3.8 | 100.7 | 0.4 | 18.2 | 2.4 | 2.9 | 130 | 3.2 | 112 | 11.7 | |
CC1 | ||||||||||||
AC from | 68 | 7.4 | 100.5 | 0.6 | 18.5 | 2.3 | 2.5 | 130 | 3.2 | 111.5 | 9.2 | 12.8 |
CC1 | ||||||||||||
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Citations (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4888192A (en) | 1972-02-04 | 1973-11-19 | ||
US4391964A (en) | 1981-02-21 | 1983-07-05 | Akzo Nv | Embedding mass of polyurethane |
US4623329A (en) | 1983-12-15 | 1986-11-18 | The Procter & Gamble Company | Drainage and infusion catheters having a capillary sleeve forming a reservoir for a fluid antimicrobial agent |
EP0311244A1 (en) | 1987-08-25 | 1989-04-12 | Kureha Kagaku Kogyo Kabushiki Kaisha | Complex of magnesium oxide and titanium dioxide as a phosphate adsorbent |
US5587157A (en) * | 1992-05-19 | 1996-12-24 | Cox; James P. | Stabilization of biowastes |
RU2137540C1 (en) | 1998-06-01 | 1999-09-20 | Петросян Эдуард Арутюнович | Sorbent regeneration method |
US6332985B1 (en) | 1999-03-29 | 2001-12-25 | Uop Llc | Process for removing toxins from bodily fluids using zirconium or titanium microporous compositions |
WO2003042098A1 (en) | 2001-11-13 | 2003-05-22 | Baxter International Inc. | Granular zirconium phosphate and methods for synthesis of same |
US20040191162A1 (en) | 2003-03-28 | 2004-09-30 | Hai Ton That | Method for processing a zirconium oxide composition in crystalline form |
JP2006519299A (en) | 2003-02-28 | 2006-08-24 | バクスター インターナショナル インコーポレイテッド | Polymer ketoaldehyde |
WO2009157877A1 (en) | 2008-06-23 | 2009-12-30 | Temasek Polytechnic | A sorbent for a dialysis device |
RU2401160C1 (en) | 2009-07-14 | 2010-10-10 | Учреждение Российской академии наук Институт химии и технологии редких элементов и минерального сырья им. И.В. Тананаева Кольского научного центра РАН (ИХТРЭМС КНЦ РАН) | Method of preparing sorbent based on titanium phosphate |
WO2011125758A1 (en) | 2010-03-31 | 2011-10-13 | 富田製薬株式会社 | Dialysis composition, hemodialysis system, and hemodialyzer |
US20130123560A1 (en) | 2009-02-09 | 2013-05-16 | The University Of Houston System | Porous solids, selective separations, removal of sulfur compounds, adsorption |
US20130260988A1 (en) | 2012-03-30 | 2013-10-03 | Basf Se | Color-Stable Superabsorbent |
US20140001112A1 (en) | 2001-11-13 | 2014-01-02 | Baxter International Inc. | Method and composition for removing uremic toxins in dialysis processes |
CN104039439A (en) | 2011-12-29 | 2014-09-10 | 费森尤斯医疗保健集团 | Materials for removal of toxins in sorbent dialysis and methods and systems using same |
US20150108069A1 (en) | 2013-10-23 | 2015-04-23 | Fresenius Medical Care Holdings, Inc. | Process For Regeneration Of Spent Zirconium Phosphate For Reuse in Sorbent Treatments |
US20150251162A1 (en) | 2013-11-26 | 2015-09-10 | Medtronic, Inc. | Zirconium phosphate recharging method and appartus |
US20150367055A1 (en) | 2014-06-24 | 2015-12-24 | Medtronic, Inc. | Method of zirconium phosphate recharging |
WO2015199768A1 (en) | 2014-06-24 | 2015-12-30 | Medtronic, Inc. | Stacked sorbent assembly |
US20160243541A1 (en) | 2013-11-26 | 2016-08-25 | Medtronic, Inc. | Zirconium phosphate and zirconium oxide recharging flow paths |
US20160243299A1 (en) | 2013-11-26 | 2016-08-25 | Medtronic, Inc. | Recharger for recharging zirconium phospahte and zirconium oxide modules |
WO2016191042A1 (en) | 2015-05-26 | 2016-12-01 | Medtronic, Inc. | Zirconium phosphate and zirconium oxide recharger control logic and operational process algorithms |
EP3269757A1 (en) | 2015-03-10 | 2018-01-17 | SDP Global Co., Ltd. | Process for producing aqueous-liquid-absorbing resin particles, aqueous-liquid-absorbing resin particles, absorbent, and absorbent article |
US20180030604A1 (en) | 2016-08-01 | 2018-02-01 | Fujitsu Limited | Carbon dioxide-reduction device |
EP3326712A1 (en) | 2016-11-29 | 2018-05-30 | Medtronic Inc. | Zirconium phosphate recharging customization |
US20180177933A1 (en) | 2015-09-16 | 2018-06-28 | Fresenius Medical Care Holdings, Inc. | Cartridges Useful In Cleaning Dialysis Solutions |
US20180214623A1 (en) | 2017-01-30 | 2018-08-02 | Medtronic, Inc. | Ganged modular recharging system |
EP3415182A1 (en) | 2017-06-15 | 2018-12-19 | Medtronic, Inc. | Zirconium phosphate disinfection recharging and conditioning |
EP3546042A1 (en) | 2018-03-30 | 2019-10-02 | Medtronic, Inc. | Precision recharging of sorbent materials using patient and session data |
US20200164128A1 (en) | 2018-11-28 | 2020-05-28 | Baxter International Inc. | Systems and methods for batch sorbent material reuse |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9616163B2 (en) * | 2012-01-04 | 2017-04-11 | Fresenius Medical Care Holdings, Inc. | Method and system of enhancing removal of toxic anions and organic solutes in sorbent dialysis |
CN107569730A (en) * | 2017-09-13 | 2018-01-12 | 华威(深圳)医疗器械有限责任公司 | A kind of device applied to haemodialysis |
CN108863937A (en) * | 2018-07-29 | 2018-11-23 | 茆振斌 | Pass through the method for titania-based complex solid catalyst preparation allantoin |
-
2018
- 2018-11-28 US US16/203,058 patent/US11925916B2/en active Active
-
2019
- 2019-11-27 SG SG11202102616PA patent/SG11202102616PA/en unknown
- 2019-11-27 WO PCT/US2019/063664 patent/WO2020113044A1/en active Search and Examination
- 2019-11-27 CN CN201980069963.8A patent/CN112969531B/en active Active
- 2019-11-27 KR KR1020217019466A patent/KR20210094608A/en active Search and Examination
- 2019-11-27 JP JP2021529042A patent/JP7306606B2/en active Active
- 2019-11-27 EP EP19824121.8A patent/EP3887034B1/en active Active
Patent Citations (37)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4888192A (en) | 1972-02-04 | 1973-11-19 | ||
US4391964A (en) | 1981-02-21 | 1983-07-05 | Akzo Nv | Embedding mass of polyurethane |
US4623329A (en) | 1983-12-15 | 1986-11-18 | The Procter & Gamble Company | Drainage and infusion catheters having a capillary sleeve forming a reservoir for a fluid antimicrobial agent |
EP0311244A1 (en) | 1987-08-25 | 1989-04-12 | Kureha Kagaku Kogyo Kabushiki Kaisha | Complex of magnesium oxide and titanium dioxide as a phosphate adsorbent |
US5587157A (en) * | 1992-05-19 | 1996-12-24 | Cox; James P. | Stabilization of biowastes |
RU2137540C1 (en) | 1998-06-01 | 1999-09-20 | Петросян Эдуард Арутюнович | Sorbent regeneration method |
US6332985B1 (en) | 1999-03-29 | 2001-12-25 | Uop Llc | Process for removing toxins from bodily fluids using zirconium or titanium microporous compositions |
WO2003042098A1 (en) | 2001-11-13 | 2003-05-22 | Baxter International Inc. | Granular zirconium phosphate and methods for synthesis of same |
US20140001112A1 (en) | 2001-11-13 | 2014-01-02 | Baxter International Inc. | Method and composition for removing uremic toxins in dialysis processes |
JP2006519299A (en) | 2003-02-28 | 2006-08-24 | バクスター インターナショナル インコーポレイテッド | Polymer ketoaldehyde |
US20040191162A1 (en) | 2003-03-28 | 2004-09-30 | Hai Ton That | Method for processing a zirconium oxide composition in crystalline form |
WO2009157877A1 (en) | 2008-06-23 | 2009-12-30 | Temasek Polytechnic | A sorbent for a dialysis device |
US20130123560A1 (en) | 2009-02-09 | 2013-05-16 | The University Of Houston System | Porous solids, selective separations, removal of sulfur compounds, adsorption |
RU2401160C1 (en) | 2009-07-14 | 2010-10-10 | Учреждение Российской академии наук Институт химии и технологии редких элементов и минерального сырья им. И.В. Тананаева Кольского научного центра РАН (ИХТРЭМС КНЦ РАН) | Method of preparing sorbent based on titanium phosphate |
WO2011125758A1 (en) | 2010-03-31 | 2011-10-13 | 富田製薬株式会社 | Dialysis composition, hemodialysis system, and hemodialyzer |
US9682184B2 (en) | 2011-12-29 | 2017-06-20 | Fresenius Medical Care Holdings, Inc. | Materials for removal of toxins in sorbent dialysis and methods and systems using same |
CN104039439A (en) | 2011-12-29 | 2014-09-10 | 费森尤斯医疗保健集团 | Materials for removal of toxins in sorbent dialysis and methods and systems using same |
US20140336568A1 (en) * | 2011-12-29 | 2014-11-13 | Fresenius Medical Care Holdings, Inc. | Materials For Removal Of Toxins In Sorbent Dialysis And Methods And Systems Using Same |
US20130260988A1 (en) | 2012-03-30 | 2013-10-03 | Basf Se | Color-Stable Superabsorbent |
US20150108069A1 (en) | 2013-10-23 | 2015-04-23 | Fresenius Medical Care Holdings, Inc. | Process For Regeneration Of Spent Zirconium Phosphate For Reuse in Sorbent Treatments |
WO2015060914A1 (en) | 2013-10-23 | 2015-04-30 | Fresenius Medical Care Holdings, Inc. | Process for regeneration of spent zirconium phosphate for reuse in sorbent treatments |
US9707329B2 (en) | 2013-10-23 | 2017-07-18 | Fresenius Medical Care Holdings, Inc. | Process for regeneration of spent zirconium phosphate for reuse in sorbent treatments |
US20160243299A1 (en) | 2013-11-26 | 2016-08-25 | Medtronic, Inc. | Recharger for recharging zirconium phospahte and zirconium oxide modules |
US20160243541A1 (en) | 2013-11-26 | 2016-08-25 | Medtronic, Inc. | Zirconium phosphate and zirconium oxide recharging flow paths |
US20150251162A1 (en) | 2013-11-26 | 2015-09-10 | Medtronic, Inc. | Zirconium phosphate recharging method and appartus |
WO2015199864A1 (en) | 2014-06-24 | 2015-12-30 | Medtronic, Inc. | Zirconium phosphate recharging method and appartus |
WO2015199768A1 (en) | 2014-06-24 | 2015-12-30 | Medtronic, Inc. | Stacked sorbent assembly |
US20150367055A1 (en) | 2014-06-24 | 2015-12-24 | Medtronic, Inc. | Method of zirconium phosphate recharging |
EP3269757A1 (en) | 2015-03-10 | 2018-01-17 | SDP Global Co., Ltd. | Process for producing aqueous-liquid-absorbing resin particles, aqueous-liquid-absorbing resin particles, absorbent, and absorbent article |
WO2016191042A1 (en) | 2015-05-26 | 2016-12-01 | Medtronic, Inc. | Zirconium phosphate and zirconium oxide recharger control logic and operational process algorithms |
US20180177933A1 (en) | 2015-09-16 | 2018-06-28 | Fresenius Medical Care Holdings, Inc. | Cartridges Useful In Cleaning Dialysis Solutions |
US20180030604A1 (en) | 2016-08-01 | 2018-02-01 | Fujitsu Limited | Carbon dioxide-reduction device |
EP3326712A1 (en) | 2016-11-29 | 2018-05-30 | Medtronic Inc. | Zirconium phosphate recharging customization |
US20180214623A1 (en) | 2017-01-30 | 2018-08-02 | Medtronic, Inc. | Ganged modular recharging system |
EP3415182A1 (en) | 2017-06-15 | 2018-12-19 | Medtronic, Inc. | Zirconium phosphate disinfection recharging and conditioning |
EP3546042A1 (en) | 2018-03-30 | 2019-10-02 | Medtronic, Inc. | Precision recharging of sorbent materials using patient and session data |
US20200164128A1 (en) | 2018-11-28 | 2020-05-28 | Baxter International Inc. | Systems and methods for batch sorbent material reuse |
Non-Patent Citations (8)
Title |
---|
Chinese Office Action dated Feb. 15, 2023 for App. No. 201980069963.8. |
India Office Action dated Jan. 20, 2023 for App. No. 202117022235. |
IPRP for PCT/US2019/063664 dated Feb. 16, 2021 (17 pages). |
Japanese Office Action dated Feb. 7, 2023 for App. No. P2021-529042. |
T Li, Langmuir, (1997), v13, p. 3570-3574. * |
Transmittal of International Search Report and Written Opinion of the International Searching Authority for PCT/US2019/063664 dated Feb. 21, 2020 (13 pages). |
Transmittal of International Search Report and Written Opinion of the International Searching Authority for PCT/US2019/063699 dated Mar. 13, 2020 (19 pages). |
Written Opinion dated Oct. 7, 2020 for PCT/US2019/063664 (7 pages). |
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